Anode material, electrochemical device and electronic device comprising the same

ABSTRACT

An anode material includes a silicon composite substrate, wherein the Dv50 of the silicon composite substrate is from 2.5 μm to 15 μm, and the particle size distribution of the silicon composite substrate meets 0.1≤Dn10/Dv50≤0.6. The anode material has good cycle performance, and the battery prepared with the anode material has good rate performance and lower swelling rate.

CROSS-REFERENCE TO RELATED APPLICATIONS

This present application is a national phase application of PCT application PCT/CN2019/118582 filed on Nov. 14, 2019, the disclosure of which is hereby incorporated by reference in its entirety.

BACKGROUND 1. Technical Field

The present application relates to the technical field of energy storage, and particularly to an anode material, an electrochemical device and an electronic device comprising the anode material, particularly, lithium-ion batteries.

2. Description of the Related Art

With the popularization of consumer electronic products, such as notebook computers, mobile phones, tablet computers, mobile power supplies, and unmanned aerial vehicles, the requirements for electrochemical devices used therein are also becoming stricter. For example, a battery is not only required to be light in weight, but is also required to have high capacity and a relatively long service life. Lithium-ion batteries have occupied the leading position in the market due to their outstanding advantages, such as high energy density, excellent safety, no memory effect, and long service life.

SUMMARY

Embodiments of the present application provide an anode material and a method for preparing the anode material, to solve at least one of the problems existing in related art to some extent. An embodiment of the present application also provides an anode using the anode material, an electrochemical device, and an electronic device.

In one embodiment, the present application provides an anode material, which comprises a silicon composite substrate, the Dv50 of the silicon composite substrate is from about 2.5 μm to 15 μm, and the particle size distribution of the silicon composite substrate meets: about 0.1≤Dn10/Dv50≤about 0.6.

In another embodiment, the present application provides an anode, which comprises an anode material according to an embodiment of the present application.

In another embodiment, the present application provides an electrochemical device, which comprises an anode according to an embodiment of the present application.

In another embodiment, the present application provides an electronic device, which comprises an electrochemical device according to an embodiment of the present application.

The anode active material of the present application has good cycle performance, and the lithium-ion battery prepared with the anode active material has good rate performance and lower swelling rate.

Additional aspects and advantages of the embodiments of the present application will be partly described or shown in the following description or interpreted by implementing the embodiments of the present application.

BRIEF DESCRIPTION OF THE DRAWINGS

Drawings necessary to describe the embodiments of the present application or the prior art will be briefly illustrated so as to facilitate the description of the embodiments of the present application. Obviously, the accompanying drawings show only some of the embodiments of the present application. For those skilled in the art, the drawings of other embodiments can still be obtained according to the structures illustrated in the drawings without any creative effort.

FIG. 1 shows a volume-basis particle size distribution curve of the anode active material in Example 2 of the present application.

FIG. 2 shows a volume-basis particle size distribution curve of the anode active material in Comparative Example 2 of the present application.

FIG. 3 illustrates a schematic structural diagram of the anode active material in an example of the present application.

FIG. 4 illustrates a schematic structural diagram of the anode active material in another example of the present application.

FIG. 5 shows an X-ray diffraction (XRD) pattern of the anode active material in Example 25 of the present application.

FIG. 6 shows an X-ray diffraction (XRD) pattern of the anode active material in Comparative Example 3 of the present application.

FIG. 7 shows a scanning electron microscopy (SEM) image of the anode active material in Example 25 of the present application.

FIG. 8 shows a scanning electron microscopy (SEM) image of the anode active material in Comparative Example 3 of the present application.

DETAILED DESCRIPTION

The embodiments of the present application will be described in detail below. The embodiments of the present application should not be interpreted as limitations to the present application.

As used in the present application, the terms “about” is used for describing and explaining a small variation. When used in connection with an event or circumstance, the term may refer to an example in which the event or circumstance occurs precisely, and an example in which the event or circumstance occurs approximately. For example, when used in connection with a value, the term may refer to a range of variation less than or equal to ±10% of the stated value, such as less than or equal to ±5%, less than or equal to ±4%, less than or equal to ±3%, less than or equal to ±2%, less than or equal to ±1%, less than or equal to ±0.5%, less than or equal to ±0.1%, or less than or equal to ±0.05%.

In the present application, Dv50 is the particle size corresponding to a cumulative volume percentage of the anode active material that is 50%, and the unit is μm.

In the present application, Dn10 is the particle size corresponding to a cumulative number percentage of the anode active material that is 10%, and the unit is μm.

In the present application, the silicon composite comprises elemental silicon, a silicon compound, a mixture of elemental silicon and a silicon compound, or a mixture of various silicides.

In addition, amounts, ratios, and other values are sometimes presented in a range format in this application. It is to be understood that such a range format is provided for the sake of convenience and simplicity, and should be understood flexibly to include not only the numerical values that are explicitly defined in the range, but also all the individual values or sub-ranges that are included in the range, as if each value and sub-range are explicitly specified.

In the detailed description and claims, a list of items connected by the term “one of” or the like means any one of the listed items. For example, if items A and B are listed, the phrase “one of A and B” means only A or only B. In another example, if items A, B, and C are listed, then the phrase “one of A, B, and C” means only A; only B; or only C. Item A may include a single or multiple elements. Item B may include a single or multiple elements. Item C may include a single or multiple elements.

In the detailed description and claims, a list of items connected by the term “at least one of” or the like means any combination of the listed items. For example, if items A and B are listed, the phrase “at least one of A and B” means only A; only B; or A and B. In another example, if items A, B, and C are listed, then the phrase “at least one of A, B, and C” means only A; only B; only C; A and B (excluding C); A and C (excluding B); B and C (excluding A); or A, B, and C. Item A may include a single or multiple elements. Item B may include a single or multiple elements. Item C may include a single or multiple elements.

I. Anode Material

An embodiment of the present application provides an anode material, which comprises a silicon composite substrate, the Dv50 of the silicon composite substrate is from 2.5 μm to 15 μm, and the particle size distribution of the silicon composite substrate meets: 0.1≤Dn10/Dv50≤0.6.

In some embodiments, the Dv50 of the silicon composite substrate is from about 2.5 μm to 15 μm. In some embodiments, the Dv50 of the silicon composite substrate is from about 2.5 μm to 10 μm. In some embodiments, the Dv50 of the silicon composite substrate is from about 3 μm to 9 μm. In some embodiments, the Dv50 of the silicon composite substrate is from about 4 μm to 7 μm.

In some embodiments, the particle size distribution of the silicon composite substrate meets: about 0.3≤Dn10/Dv50≤about 0.5. In some embodiments, the particle size distribution of the silicon composite substrate meets: Dn10/Dv50=about 0.35 or about 0.4.

In some embodiments, the silicon composite substrate comprises a silicon-containing substance. The silicon-containing substance in the silicon composite substrate can form a composite with one or more of other substances than the silicon-containing substance in the anode material. In some embodiments, the silicon composite substrate comprises particles that can intercalate and deintercalate lithium ions.

In some embodiments, the silicon composite substrate comprises SiO_(x), wherein about 0.6≤x≤about 1.5.

In some embodiments, the silicon composite substrate comprises nano-Si crystalline grains, SiO, SiO₂, or any combination thereof.

In some embodiments, the particle size of the nano-Si crystalline grains is less than about 100 nm. In some embodiments, the particle size of the nano-Si crystalline grains is less than about 50 nm. In some embodiments, the particle size of the nano-Si crystalline grains is less than about 20 nm. In some embodiments, the particle size of the nano-Si crystalline grains is less than about 5 nm. In some embodiments, the particle size of the nano-Si crystalline grains is less than about 2 nm. In some embodiments, the particle size of the nano-Si crystalline grains is less than about 0.5 nm.

In some embodiments, the anode material further comprises an oxide MeO_(y) layer coating at least a portion of the silicon composite substrate, wherein Me includes at least one of Al, Si, Ti, Mn, V, Cr, Co or Zr, and y is about 0.5-3; and wherein the oxide MeO_(y) layer comprises a carbon material.

In some embodiments, the oxide MeO_(y) includes Al₂O₃, SiO₂, TiO₂, Mn₂O₃, MnO₂, CrO₃, Cr₂O₃, CrO₂, V₂O₅, VO, CoO, Co₂O₃, Co₃O₄, ZrO₂ or any combination thereof.

In some embodiments, the carbon material in the oxide MeO_(y) layer includes amorphous carbon, carbon nanotubes, carbon nanoparticles, carbon fibers, graphene, or any combination thereof. In some embodiments, the amorphous carbon is a carbon material obtained by sintering a carbon precursor at high temperature. In some embodiments, the carbon precursor includes polyvinylpyrrolidone, sodium carboxymethyl cellulose, polyvinyl alcohol, polypropylene, phenolic resin, polyester resin, polyamide resin, epoxy resin, polyurethane, polyacrylic resin or any combination thereof.

In some embodiments, the thickness of the oxide MeO_(y) layer is about 1 nm to 1000 nm. In some embodiments, the thickness of the oxide MeO_(y) layer is about 10 nm to 900 nm. In some embodiments, the thickness of the oxide MeO_(y) layer is about 20 nm to 800 nm. In some embodiments, the thickness of the oxide MeO_(y) layer is about 1 nm to 20 nm. In some embodiments, the thickness of the oxide MeO_(y) layer is about 2 nm, about 5 nm, about 10 nm, about 15 nm, about 20 nm, or about 50 nm.

In some embodiments, based on the total weight of the anode material, the weight percentage of the Me element is about 0.01 wt % to 1 wt %. In some embodiments, based on the total weight of the anode material, the weight percentage of the Me element is about 0.02 wt % to 1 wt %. In some embodiments, based on the total weight of the anode material, the weight percentage of the Me element is about 0.03 wt % to 0.9 wt %. In some embodiments, based on the total weight of the anode material, the weight percentage of the Me element is about 0.05 wt %, about 0.1 wt %, about 0.2 wt %, about 0.3 wt %, about 0.4 wt %, about 0.5 wt %, about 0.6 wt %, about 0.7 wt % or about 0.8 wt %.

In some embodiments, based on the total weight of the anode material, the weight percentage of the carbon material in the oxide MeO_(y) layer is about 0.05 wt % to 1 wt %. In some embodiments, based on the total weight of the anode material, the weight percentage of the carbon material in the oxide MeO_(y) layer is about 0.1 wt % to 0.8 wt %. In some embodiments, based on the total weight of the anode material, the weight percentage of the carbon material in the oxide MeO_(y) layer is about 0.2 wt % to 0.7 wt %. In some embodiments, based on the total weight of the anode material, the weight percentage of the carbon material in the oxide MeO_(y) layer is about 0.3 wt %, about 0.4 wt %, about 0.5 wt %, about 0.6 wt %, about 0.7 wt % or about 0.8 wt %.

In some embodiments, the anode material further comprises a polymer layer that coats at least a portion of the oxide MeO_(y) layer, wherein the polymer layer comprises a carbon material.

In some embodiments, the polymer layer comprises polyvinylidene fluoride and its derivatives, carboxymethyl cellulose and its derivatives, sodium carboxymethyl cellulose and its derivatives, polyvinylpyrrolidone and its derivatives, polyacrylic acid and its derivatives, polystyrene-butadiene rubber, polyacrylamide, polyimide, polyamideimide or any combination thereof.

In some embodiments, the carbon material in the polymer layer includes carbon nanotubes, carbon nanoparticles, carbon fibers, graphene, or any combination thereof.

In some embodiments, based on the total weight of the anode material, the weight percentage of the polymer layer is about 0.1 wt % to 10 wt %. In some embodiments, based on the total weight of the anode material, the weight percentage of the polymer layer is about 0.2 wt % to 8 wt %. In some embodiments, based on the total weight of the anode material, the weight percentage of the polymer layer is about 0.3 wt % to 7 wt %. In some embodiments, based on the total weight of the anode material, the weight percentage of the polymer layer is about 1 wt %, about 1.5 wt %, about 2 wt %, about 4 wt %, about 5 wt % or about 6 wt %.

In some embodiments, the thickness of the polymer layer is about 2 nm to 100 nm. In some embodiments, the thickness of the polymer layer is about 10 nm to 90 nm. In some embodiments, the thickness of the polymer layer is about 15 nm to 80 nm. In some embodiments, the thickness of the polymer layer is about 5 nm, about 20 nm, about 25 nm, about 45 nm, about 55 nm or about 75 nm.

In some embodiments, the anode material has a specific surface area of about 1 m²/g to 50 m²/g. In some embodiments, the anode material has a specific surface area of about 1 m²/g to 30 m²/g. In some embodiments, the anode material has a specific surface area of about 1 m²/g to 10 m²/g. In some embodiments, the anode material has a specific surface area of about 1 m²/g, about 5 m²/g, or about 10 m²/g.

In some embodiments, in the X-ray diffraction pattern of the anode material, the highest intensity at 2θ within the range of about 27.0° to 30.0° is I₂, and the highest intensity at 2θ within the range of about 20.0° to 22.0° is I₁, wherein about 0≤I₂/I₁≤about 1.

In some embodiments, in the X-ray diffraction pattern of the anode material, the highest intensity at 2θ of about 28.4° is I₂, and the highest intensity at 2θ of about 21.0° is I₁, wherein about 0.1<I₂/I₁≤about 1. In some embodiments, I₂/I₁ is 0.2, 0.4 or 0.5.

II. Preparation Method of Anode Material

An embodiment of the present application provides a method for preparing any of the anode material as described above, the method comprises: grading silicon oxide SiO_(x) to obtain an anode material having a particle size distribution meeting: 0.1≤Dn10/Dv50≤0.6, where 0.6≤x≤1.5.

In some embodiments, the grading includes air flow classification.

In some embodiments, the method further comprises a step of coating an oxide MeO_(y) layer, comprising:

-   -   (1) forming the graded solid, a carbon precursor and an oxide         precursor MeT_(n) into a mixed solution in the presence of an         organic solvent and deionized water;     -   (2) drying the mixed solution to obtain powder; and     -   (3) sintering the powder at about 200° C. to 900° C. for about         0.5 hr to 20 hr, to obtain an anode material with an oxide         MeO_(y) layer on the surface,

wherein y is about 0.5 to 3,

wherein Me includes at least one of Al, Si, Ti, Mn, Cr, V, Co or Zr,

wherein T includes at least one of methoxy, ethoxy, isopropoxy or halogen, and

wherein n is 1, 2, 3 or 4.

In some embodiments, the oxide precursor MeT_(n) includes isopropyl titanate, aluminum isopropoxide, or a combination thereof.

In some embodiments, the carbon material includes amorphous carbon, carbon nanotubes, carbon nanoparticles, carbon fibers, graphene, or any combination thereof. In some embodiments, the amorphous carbon is a carbon material obtained by sintering a carbon precursor at high temperature. In some embodiments, the carbon precursor includes polyvinylpyrrolidone, sodium carboxymethyl cellulose, polyvinyl alcohol, polypropylene, phenolic resin, polyester resin, polyamide resin, epoxy resin, polyurethane, polyacrylic resin or any combination thereof.

In some embodiments, the sintering temperature is about 250° C. to 800° C. In some embodiments, the sintering temperature is about 300° C. to 700° C. In some embodiments, the sintering temperature is about 400, about 500° C. or about 600° C.

In some embodiments, the sintering time is about 1 hr to 18 hr. In some embodiments, the sintering time is about 1 hr to 16 h. In some embodiments, the sintering time is about 1 hr to 12 hr. In some embodiments, the sintering time is about 1.5 hr to 6 hr. In some embodiments, the sintering time is about 1.5 hr, about 2.5 hr, about 3.5 hr, about 5 hr or about 6 hr.

In some embodiments, the organic solvent includes at least one of ethanol, methanol, n-hexane, N,N-dimethylformamide, pyrrolidone, acetone, toluene, isopropanol or n-propanol. In some embodiments, the organic solvent is ethanol.

In some embodiments, the halogen includes F, Cl, Br, or a combination thereof.

In some embodiments, the sintering is carried out under an inert gas atmosphere. In some embodiments, the inert gas includes nitrogen, argon, or a combination thereof.

In some embodiments, the drying is spray drying and the drying temperature is about 100° C. to 300° C.

In some embodiments, the method further comprises a step of coating the polymer layer, comprising:

-   -   (1) dispersing the above-mentioned graded solid or the anode         material with the oxide MeO_(y) layer on the surface, a carbon         material and a polymer at a high speed in a solvent for 1-15 hrs         to obtain a suspension; and     -   (2) removing the solvent from the suspension.

In some embodiments, the polymer comprises polyvinylidene fluoride and its derivatives, carboxymethyl cellulose and its derivatives, sodium carboxymethyl cellulose and its derivatives, polyvinylpyrrolidone and its derivatives, polyacrylic acid and its derivatives, polystyrene-butadiene rubber, polyacrylamide, polyimide, polyamideimide or any combination thereof.

In some embodiments, the carbon material includes carbon nanotubes, carbon nanoparticles, carbon fibers, graphene, or any combination thereof.

In some embodiments, the solvent includes water, ethanol, methanol, tetrahydrofuran, acetone, chloroform, N-methylpyrrolidone, dimethylformamide, dimethylacetamide, toluene, xylene, or any combination thereof.

In some embodiments, the silicon oxide SiO_(x) may be a commercial silicon oxide, or a silicon oxide SiO_(x) prepared according to a method of the present invention. In the X-ray diffraction pattern of the silicon oxide SiO_(x) prepared according to a method of the present invention, the highest intensity at 2θ within the range of about 27.0°-30.0° is I₂, and the highest intensity at 2θ within the range of about 20.0°-22.0° is I₁, wherein about 0<I₂/I₁≤about 1. In some embodiments, I₂/I₁ is about 0.2, about 0.4 or about 0.5.

In the present invention, the method for preparing a silicon oxide SiO_(x) meeting about 0<I₂/I₁≤about 1 comprises:

-   -   (1) mixing silicon dioxide and metal silicon powder at a molar         ratio of about 1:6-6:1 to obtain a mixed material;     -   (2) under about 10⁻⁴-10⁻¹ kPa, heating the mixed material for         about 1-25 hr at a temperature ranging from about 1100° C. to         1800° C. to obtain a gas;     -   (3) condensing the gas to obtain a solid;     -   (4) crushing and screening the solid; and     -   (5) heat-treating the solid at a temperature ranging from about         400° C. to 1500° C. for about 0.5 hr to 24 hr, and cooling to         obtain a silicon oxide SiO_(x) meeting about 0<I₂/I₁≤about 1.

In some embodiments, the molar ratio of silicon dioxide to the metal silicon powder is about 1:4-4:1. In some embodiments, the molar ratio of silicon dioxide to the metal silicon powder is about 1:3-3:1. In some embodiments, the molar ratio of silicon dioxide to the metal silicon powder is about 1:2-2:1. In some embodiments, the molar ratio of silicon dioxide to the metal silicon powder is about 1:1, about 1.5:1 or about 2.5:1.

In some embodiments, the pressure is in the range of about 10⁻⁴ kP to 10⁻¹ kPa. In some embodiments, the pressure is about 1 Pa, about 10 Pa, about 20 Pa, about 30 Pa, about 40 Pa, about 50 Pa, about 60 Pa, about 70 Pa, about 80 Pa, about 90 Pa or about 100 Pa.

In some embodiments, the heating temperature is about 1100° C. to 1500° C. In some embodiments, the heating temperature is about 1150° C., about 1200° C., about 1250° C. or about 1400° C.

In some embodiments, the heating temperature is about 1 hr to 20 hr. In some embodiments, the heating temperature is about 5 hr to 15 hr. In some embodiments, the heating time is about 2 hr, about 4 hr, about 6 hr, about 8 hr, about 10 hr, about 12 hr, about 14 hr, about 16 hr or about 18 hr.

In some embodiments, the mixing is performed in a ball mill, a V-type mixer, a three-dimensional mixer, an airflow mixer, or a horizontal mixer.

In some embodiments, the heating and heat-treating are carried out under an inert gas atmosphere. In some embodiments, the inert gas includes nitrogen, argon, helium, or a combination thereof.

In some embodiments, after screening, the method further comprises a heat-treatment step.

In some embodiments, the heat-treatment temperature is about 500° C. to 1500° C. In some embodiments, the heat-treatment temperature is about 400° C. to 1200° C. In some embodiments, the heat-treatment temperature is about 600° C., about 800° C. or about 1000° C.

In some embodiments, the heat-treatment time is about 1 hr to 24 hr. In some embodiments, the thermal treatment time is about 2 hr to 12 hr. In some embodiments, the thermal treatment time is about 5 hr, about 10 hr or about 15 hr.

FIG. 1 shows a volume-basis particle size distribution curve of the anode active material in Example 2. It can be seen from FIG. 1 that the particle size distribution of the anode active material particles of Example 2 is relatively uniform, and narrow. The lithium-ion battery prepared with the anode active material of Example 2 shows a satisfactory cycle performance and swelling resistance.

FIG. 2 shows a volume-basis particle size distribution curve of the anode active material in Comparative Example 2. It can be seen from FIG. 2 that the anode active material of Comparative Example 2 has a certain number of small particles, so the cycle performance is poor. The presence of small fine particles accelerates the etching of the particles by the electrolytic solution and thus accelerates the deterioration of the cycle performance. Moreover, since the small particles are quickly etched by the electrolytic solution, a large amount of by-products are produced on the surface, so the swelling resistance of the lithium-ion battery prepared therefrom is worse than the swelling resistance of the lithium-ion battery prepared with the anode active material of Comparative Example 2.

FIG. 3 illustrates a schematic structural diagram of an anode active material in an example of the present application. The inner layer 1 is a silicon composite substrate, and the outer layer 2 is an oxide MeO_(y) layer containing the carbon material.

The oxide MeO_(y) layer coating the silicon composite substrate can act as an HF trapping agent, and the oxide can react with HF in the electrolytic solution to reduce the content of HF in the electrolytic solution during the cycle process, and reduce the etching of HF on the surface of the silicon material, thereby further improving the cycle performance of the material. Doping a carbon material in the oxide MeO_(y) layer is beneficial for the formation of the lithium-ion conductors after intercalation of the lithium during the first charge and discharge process, and is beneficial for achieving the conduction of ions. In addition, doping a certain amount of carbon in the oxide MeO_(y) layer can enhance the conductivity of the anode active material.

FIG. 4 is a schematic structural diagram of an anode active material in another example of the present application. The inner layer 1 is a silicon composite substrate, the middle layer 2 is an oxide MeO_(y) layer containing a carbon material, and the outer layer 3 is a polymer layer containing a carbon material. The anode active material of the present application may only have the silicon composite substrate and the polymer layer, but without the MeO_(y) layer. That is, the polymer layer of the present application can be directly coated on the surface of the silicon composite substrate.

When a polymer layer containing carbon nanotubes (CNT) is coated on the surface of the anode active material, the CNTs can be bound to the surface of the anode active material by the polymer, which is beneficial for the improvement of the interface stability of the CNTs on the surface of the anode active material, thereby improving cycle performance.

FIG. 5 shows an X-ray diffraction (XRD) pattern of an anode active material in Example 25 of the present application. As can be seen from FIG. 5, in the X-ray diffraction pattern of the anode active material, the highest intensity at 2θ within the range of 28.0° to 29.0° is I₂, and the highest intensity at 2θ within the range of 20.5° to 21.5° is I₁, wherein 0<I₂/I₁≤1. The I₂/I₁ value reflects the influence degree of disproportionation to the material. The larger the I₂/I₁ value is, the larger the size of the nano-silicon crystalline grains inside the anode active material will be. When the I₂/I₁ value is greater than 1, the stress in a local region of the anode active material will sharply increase during intercalation of the lithium, so that the structure of the anode active material is degraded during the cycle process. In addition, due to the generation of the distribution of nanocrystals, the diffusion capacity of the ions in the grain boundary during diffusion of the ion process will be affected. The inventors of the present application finds that when the I₂/I₁ value meets 0<I₂/I₁≤1, the anode active material has good cycle performance, and the lithium-ion battery prepared with the same has good swelling resistance.

FIG. 6 shows an X-ray diffraction (XRD) pattern of an anode active material in Comparative Example 3 of the present application. It can be seen from FIG. 6 that the anode active material of Comparative Example 3 has an I₂/I₁ value that is significantly greater than 1. Compared with the anode active material of Example 25, the anode active material of Comparative Example 3 has poor cycle performance, and the lithium-ion battery prepared with the same has a high swelling rate and poor rate performance

FIGS. 7 and 8 show scanning electron microscopy (SEM) images of the anode active materials in Example 25 and Comparative Example 3, respectively. The particle size distribution can be visually observed from FIGS. 7 and 8. FIG. 8 shows that a certain number of small particles are present in the anode active material of Comparative Example 3.

III. Anode

The embodiments of the present application provide an anode. The anode includes a current collector and an anode active material layer located on the current collector. The anode active material layer includes an anode material according to the embodiments of the present application.

In some embodiments, the anode active material layer comprises a binder. In some embodiments, the binder includes, but is not limited to, polyvinyl alcohol, carboxymethyl cellulose, hydroxypropyl cellulose, diacetyl cellulose, polyvinyl chloride, carboxylated polyvinyl chloride, polyvinyl fluoride, a polymer containing ethylene oxide, polyvinylpyrrolidone, polyurethane, polytetrafluoroethylene, poly(1,1-vinylidene fluoride), polyethylene, polypropylene, styrene-butadiene rubber, acrylic styrene butadiene rubber, epoxy resin, Nylon and so on.

In some embodiments, the anode active material layer comprises a conductive material. In some embodiments, the conductive material includes, but is not limited to, natural graphite; artificial graphite; carbon black; acetylene black; Ketjen black; carbon fibers; a metal powder; metal fibers; copper; nickel; aluminum; silver; or polyphenylene derivatives.

In some embodiments, the current collector includes, but is not limited to, a copper foil, a nickel foil, a stainless steel foil, a titanium foil, nickel foam, copper foam, or a polymeric substrate coated with a conductive metal.

In some embodiments, the anode can be obtained by mixing an active material, a conductive material, and a binder in a solvent to prepare an active material composition, and coating the active material composition on a current collector.

In some embodiments, the solvent may include, but is not limited to, N-methylpyrrolidone or the like.

IV. Cathode

A material capable of being applied to a cathode in the embodiment of the present application, a composition and a preparation method thereof include any technology disclosed in prior art. In some embodiments, the cathode is a cathode disclosed in US Patent Application U.S. Pat. No. 9,812,739B, which is incorporated into the present application by full text reference.

In some embodiments, the cathode includes a current collector and a cathode active material layer on the current collector.

In some embodiments, the cathode active material includes, but is not limited to, lithium cobalt oxide (LiCoO2), lithium nickel cobalt manganese (NCM) ternary material, lithium iron phosphate (LiFePO4), or lithium manganese oxide (LiMn2O4).

In some embodiments, the cathode active material layer further comprises a binder, and optionally a conductive material. The binder improves the binding of the cathode active material particles to each other and the binding of the cathode active material to the current collector.

In some embodiments, the binder includes, but is not limited to, polyvinyl alcohol, hydroxypropyl cellulose, diacetyl cellulose, polyvinyl chloride, carboxylated polyvinyl chloride, polyvinyl fluoride, a polymer containing ethylene oxide, polyvinylpyrrolidone, polyurethane, polytetrafluoroethylene, poly(1,1-vinylidene fluoride), polyethylene, polypropylene, styrene-butadiene rubber, acrylated styrene butadiene rubber, epoxy resins, Nylon and so on.

In some embodiments, the conductive material includes, but is not limited to, a carbon-based material, a metal based material, a conductive polymer, and a mixture thereof. In some embodiments, the carbon-based material is selected from natural graphite, artificial graphite, carbon black, acetylene black, Ketjen black, carbon fiber, or any combinations thereof. In some embodiments, the metal based material is selected from metal powders, metal fibers, copper, nickel, aluminum, and silver. In some embodiments, the conductive polymer is a polyphenylene derivative.

In some embodiments, the current collector includes, but is not limited to, aluminum.

The cathode may be prepared by a preparation method well known in the art. For example, the cathode can be obtained by the following method: mixing an active material, a conductive material and a binder in a solvent to prepare an active material composition, and coating the active material composition on a current collector. In some embodiments, the solvent may include, but is not limited to, N-methylpyrrolidone or the like.

V. Electrolytic solution

An electrolytic solution that can be used in the embodiments of the present application may be an electrolytic solution known in prior art.

In some embodiments, the electrolytic solution comprises an organic solvent, a lithium salt, and an additive. The organic solvent used in the electrolytic solution according to the present application may be any organic solvent known in the art and capable of serving as a solvent of the electrolytic solution. The electrolyte used in the electrolytic solution according to the present application is not limited, and may be any electrolyte known in the art. The additive used in the electrolytic solution according to the present application may be any additive known in the art and capable of serving as an additive of the electrolytic solution.

In some embodiments, the organic solvent includes, but is not limited to, ethylene carbonate (EC), propylene carbonate (PC), diethyl carbonate (DEC), ethyl methyl carbonate (EMC), dimethyl carbonate (DMC), propylene carbonate or ethyl propionate.

In some embodiments, the lithium salt includes at least one of an organic lithium salt or an inorganic lithium salt.

In some embodiments, the lithium salt includes, but is not limited to, lithium hexafluorophosphate (LiPF₆), lithium tetrafluoroborate (LiBF₄), lithium difluorophosphate (LiPO₂F₂), lithium bis(trifluoromethanesulfonyl)imide LiN(CF₃SO₂)₂ (LiTFSI), lithium bis(fluorosulfonyl)imide Li(N(SO₂F)₂ (LiFSI), lithium bis(oxalato)borate LiB(C₂O₄)₂ (LiBOB), or lithium difluoro(oxalato)borate LiBF₂(C₂O₄) (LiDFOB).

In some embodiments, the concentration of the lithium salt in the electrolytic solution is about 0.5 mol/L to 3 mol/L, about 0.5 mol/L to 2 mol/L, or about 0.8 mol/L to 1.5 mol/L.

VI. Separator

In some embodiments, a separator is provided between the cathode and the anode to prevent a short circuit. The material and shape of the separator that can be used in the embodiment of the present application are not particularly limited, and may be any of the techniques disclosed in the prior art. In some embodiments, the separator includes a polymer or an inorganic substance or the like formed by a material which is stable in the electrolytic solution of the present application.

For example, the separator may include a substrate layer and a surface treatment layer. The substrate layer is a non-woven fabric, a film, or a composite film having a porous structure. The material of the substrate layer is selected from at least one of polyethylene, polypropylene, polyethylene terephthalate, and polyimide. Specifically, a porous polypropylene film, a porous polyethylene film, a polypropylene nonwoven fabric, a polyethylene non-woven fabric, and a porous polypropylene-polyethylene-polypropylene composite film may be used.

At least one surface of the substrate layer is provided with a surface treatment layer. The surface treatment layer may be a polymer layer or an inorganic layer, or a layer formed by mixing the polymer and the inorganic material.

The inorganic layer comprises inorganic particles and a binder. The inorganic particles are one or a combination of several selected from the group consisting of alumina, silicon dioxide, magnesia, titania, hafnium dioxide, tin oxide, cerium dioxide, nickel oxide, zinc oxide, calcium oxide, zirconia, yttria, silicon carbide, eboehmite, aluminum hydroxide, magnesium hydroxide, calcium hydroxide and barium sulfate, or a combination of more than one thereof. The binder is one selected from the group consisting of polyvinylidene fluoride, copolymer of vinylidene fluoride-hexafluoropropylene, polyamide, polyacrylonitrile, polyacrylate ester, polyacrylic acid, polyacrylate salt, polyvinylpyrrolidone, polyvinyl ether, polymethyl methacrylate, polytetrafluoroethylene, and polyhexafluoropropylene.

The polymer layer contains a polymer, and the material of the polymer is selected from at least one of polyamide, polyacrylonitrile, an acrylate polymer, polyacrylic acid, polyacrylate, polyvinylpyrrolidone, polyvinyl ether, polyvinylidene fluoride or poly(vinylidene fluoride-hexafluoropropylene).

VII. Electrochemical Device

The embodiments of the present application provide an electrochemical device including any device that undergoes an electrochemical reaction.

In some embodiments, the electrochemical device of the present application includes a cathode having a cathode active material capable of occluding and releasing metal ions; an anode according to an embodiment of the present application; an electrolytic solution; and a separator located between the cathode and the anode.

In some embodiments, the electrochemical device of the present application includes, but is not limited to, all kinds of primary batteries, secondary batteries, fuel cells, solar cells, or capacitors.

In some embodiments, the electrochemical device is a lithium secondary battery.

In some embodiments, the lithium secondary battery includes, but is not limited to, a lithium metal secondary battery, a lithium-ion secondary battery, a lithium polymer secondary battery or a lithium-ion polymer secondary battery.

VIII. Electronic Device

The electronic device of the present application may be any device using the electrochemical device according to an embodiment of the present application.

In some embodiments, the electronic device comprises, but is not limited to, notebook computers, pen-input computers, mobile computers, e-book players, portable phones, portable fax machines, portable copy machine, portable printers, stereo headphones, video recorders, liquid crystal display television, portable cleaners, portable CD players, minidisc players, transceivers, electronic notebooks, calculators, memory cards, portable recorders, radios, backup power supplies, motors, vehicles, motorcycles, power-assisted scooters, bicycles, lighting fixture, toys, game consoles, clocks, electric tools, flash light, cameras, large household batteries, or lithium-ion capacitors, and the like.

The lithium-ion battery is taken as an example and the preparation of the lithium-ion battery is described in conjunction with specific embodiments. Those skilled in the art would understand that the preparation method described in the present application is only an example, and any other suitable preparation methods are within the scope of the present application.

EXAMPLES

The following describes embodiments of the lithium-ion batteries battery according to the present application and comparative examples for performance evaluation.

Performance evaluation method for anode active materials

I. Test Method for Powder Properties of Anode Active Materials

(1) Microscopic Morphology Observation of Powder Particles:

The microscopic morphology of powder was observed by scanning electron microscopy to characterize the coating on the surface of the material. The test instrument was an OXFORD EDS (X-max-20 mm²), the acceleration voltage was 15 KV, the focal length was adjusted, the observation was made at 50K high magnification, and the agglomeration condition of the particles was observed at a low magnification of 500 to 2000.

(2) Specific Surface Area Test:

At a constant low temperature, after the adsorption amounts of gas on a solid surface at different relative pressures were measured, the adsorption amount of a monomolecular layer of a test sample was obtained based on the Brunauer-Emmett-Teller adsorption theory and its formula (BET formula), thereby calculating the specific surface area of the solid.

About 1.5 g to 3.5 g of the powder sample was loaded into a test sample tube of a TriStar II 3020, and then was degassed at about 200° C. for 120 min, and then tested.

(3) Particle Size Test:

About 0.02 g of the powder sample was added to a 50 ml clean beaker, about 20 ml of deionized water was added, and then a few drops of 1% surfactant were added to disperse the powder completely in water. Performing an ultrasonic treatment for 5 min in a 120 W ultrasonic cleaning machine, the particle size distribution was then measured by a Master Sizer 2000.

(4) Carbon Content Test:

The sample was heated and burned in a high-frequency furnace at a high temperature under an oxygen-enriched atmosphere to oxidize carbon and sulfur into carbon dioxide and sulfur dioxide, respectively. The gas was allowed to enter a corresponding absorption tank after treatment, and the corresponding infrared radiation was absorbed and converted into a corresponding signal by the detector. This signal was sampled by a computer, and converted into a value proportional to the concentration of carbon dioxide and sulfur dioxide after linear correction, and then the values throughout the entire analysis process were accumulated. After the analysis was completed, the accumulated value was divided by the weight in the computer, and then multiplied by the correction coefficient, and the blank was subtracted, to obtain the percentage content of carbon and sulfur in the sample. The sample was tested using a Shanghai Dekai HCS-140 high-frequency infrared carbon-sulfur analyzer.

(5) XRD Test:

1 g to 2.0 g of the sample was added to a groove of a glass sample holder, compacted and flattened with a glass sheet, and tested using a Brook D8 X-ray diffractometer according to JJS K 0131-1996 “General rules for X-ray diffraction analysis”. The test voltage was 40 kV, the current was 30 mA, the scanning angle was in the range of 10-85°, the scanning step size was 0.0167°, and the time for each step was 0.24 s. An XRD pattern was obtained, from which the highest intensity I₂ at 2θ of 28.4° and the highest intensity I₁ at 2θ of 21.0° were obtained, and the ratio of I₂/I₁ was calculated.

(6) Metal Element Test:

A certain amount of the sample was weighed, added with an amount of concentrated nitric acid, and digested under microwave to obtain a solution. The obtained solution and filter residue were washed multiple times and diluted to a certain volume. The plasma intensities of the metal elements were tested by ICP-OES, the metal contents in the solution were calculated according to the standard curves of the tested metals, and then the amounts of the metal elements contained in the material were calculated.

The weight percentage of each substance in the following tables was calculated based on the total weight of the anode active material.

II. Test Method of Electrical Properties of Anode Active Materials

1. Test Method for Button Battery

Under a dry argon atmosphere, LiPF₆ was added to a mixed solvent of propylene carbonate (PC), ethylene carbonate (EC), and diethyl carbonate (DEC) (at a weight ratio of about 1:1:1), and then uniformly mixed, wherein the concentration of LiPF₆ was about 1.15 mol/L. About 7.5 wt % of fluoroethylene carbonate (FEC) was added, and mixed uniformly to obtain an electrolytic solution.

The anode active material obtained in the examples and comparative examples, conductive carbon black and a modified polyacrylic acid (PAA) binder were added to deionized water at a weight ratio of about 80:10:10, and were stirred to form a slurry. A scraper was used for coating to form a coating layer with a thickness of 100 μm. The coating layer was dried in a vacuum drying oven at about 85° C. for about 12 hr, and then cut into a wafer with a diameter of about 1 cm with a punching machine in a dry environment. In a glove box, a lithium metal sheet was used as a counter electrode, and a Ceglard composite membrane was used as a separator, and an electrolytic solution was added to assemble a button battery. A LAND series battery test was used to perform charge and discharge tests on the battery to test the charge and discharge capacity of the battery. The first Coulombic efficiency was the ratio of the charge capacity to the discharge capacity.

2. Whole Battery Test

(1) Preparation of the Lithium-Ion Battery

Preparation of the Cathode:

LiCoO₂, conductive carbon black and polyvinylidene fluoride (PVDF) were fully stirred and mixed in an N-methylpyrrolidone solvent system at a weight ratio of about 95%:2.5%:2.5%, to prepare a cathode slurry. The cathode slurry prepared was coated on an aluminum foil as a cathode current collector, dried, and then cold-pressed to obtain the cathode.

Preparation of the Anode:

Graphite, the anode active material prepared according to the examples and comparative examples, a conductive agent (conductive carbon black, Super P®), and the PAA binder were mixed at a weight ratio of about 70%:15%:5%:10%, an appropriate amount of water was added, and kneaded at a solid content of about 55 wt % to 70 wt %. An appropriate amount of water was added to adjust the viscosity of the slurry to about 4000 Pa·s to 6000 Pa·s, to prepare an anode slurry.

The anode slurry prepared was coated on a copper foil as an anode current collector, dried, and then cold-pressed to obtain the anode.

Preparation of the Electrolytic Solution

Under a dry argon atmosphere, LiPF₆ was added to a mixed solvent of propylene carbonate (PC), ethylene carbonate (EC), and diethyl carbonate (DEC) (at a weight ratio of about 1:1:1), and uniformly mixed, wherein the concentration of LiPF₆ was about 1.15 mol/L. About 7.5 wt % of fluoroethylene carbonate (FEC) was added, and uniformly mixed to obtain an electrolytic solution.

Preparation of the Separator

A porous PE polymer film was used as a separator.

Preparation of the lithium-ion battery

The cathode, separator, and anode were stacked in an order such that the separator was located between the cathode and anode to isolate the cathode and anode, and a battery cell was obtained by winding. The battery cell was placed in an outer package, and the electrolytic solution was injected, and the outer package was packaged. After formation, degassing, trimming and other processes, the lithium-ion battery was obtained.

(2) Cycle Performance Test:

The test temperature was 25/45° C. The battery was charged to 4.4 V at a constant current of 0.7 C and then charged to 0.025 C at a constant voltage, allowed to stand for 5 min, and discharged to 3.0 V at 0.5 C. The capacity obtained in this step was the initial capacity. The cycle of charge at 0.7 C/discharge at 0.5 C was repeated, and ratio of the capacity of each step to the initial capacity was obtained, from which a capacity attenuation curve was obtained. The cycle number at 25° C. to a capacity retention rate of 90% was recorded as the room-temperature cycle performance of the battery, and the cycle number at 45° C. to a capacity retention rate of 80% was recorded as the high-temperature cycle performance of the battery. The cycle performances of the materials were compared by comparing the cycle number s in the above two conditions.

(3) Discharge Rate Test:

At 25° C., the battery was discharged to 3.0V at 0.2 C, allowed to stand for 5 min, charged to 4.45V at 0.5 C, charged to 0.05 C at a constant voltage, and allowed to stand for 5 min. The discharge rate was adjusted, and the battery was respectively discharged at 0.2 C, 0.5 C, 1 C, 1.5 C, and 2.0 C, to obtain the discharge capacity. The capacity obtained at each rate and the capacity obtained at 0.2 C were compared. The rate performance was compared by comparing the ratios at 2 C and 0.2 C.

(4) Swelling Rate Test of a Battery after Full Charge

The thickness of a fresh battery of half charge (50% state of charge (SOC)) was measured by a screw micrometer. After 400 cycles, the thickness of the battery of full charge (100% SOC) was measured by a screw micrometer, and compared with the thickness of the initial fresh battery of half charge (50% SOC), to obtain the swelling rate of the fully charged (100% SOC) battery at this time.

III. Preparation of the Anode Active Material

1. A commercially-available silicon oxide SiO_(x) (0.6≤x≤1.5, Dv50: about 5 μm) is graded to prepare the anode active materials of Examples 1-3 and Comparative Examples 1-2.

Table 1-1 and Table 1-2 show the performance test results of the anode active materials in Examples 1-3 and Comparative Examples 1 and 2.

TABLE 1-1 Carbon Specific Capacity per content surface area/ gram * First Dv50 (μm) Dn10/Dv50 (wt %) (m² · g⁻¹) (mAh · g⁻¹) efficiency Example 1 5.0 0.3 0.028 1.56 1672 68.8% Example 2 5.0 0.5 0.030 1.42 1683 69.0% Example 3 5.0 0.6 0.029 1.23 1682 69.2% Comparative 5.0 0.05 0.031 3.78 1681 68.1% Example 1 Comparative 5.0 0.7 0.028 1.18 1680 68.2% Example 2

TABLE 1-2 Number of Number of Swelling rate cycles at cycles at of battery 25° C. 45° C. after 400 Rate No. to 90% to 80% cycles at 45° C. performance Example 1 375 350 8.0% 84.6% Example 2 390 375 7.9% 84.8% Example 3 393 390 7.8% 84.4% Comparative 274 302 7.8% 85.0% Example 1 Comparative 350 320 8.4% 84.8% Example 2

Dn10/Dv50 is the ratio of the diameter Dn10 corresponding to a cumulative number percentage being 10% in the number-basis distribution curve to the diameter Dv50 corresponding to a cumulative volume percentage being 50% in the volume basis distribution curve obtained by the laser scattering particle size analyzer. The larger the Dn10/Dv50 value is, the fewer small particles there are in the material.

As can be seen from the test results of Examples 1-3 and Comparative Examples 1 and 2, the lithium-ion battery prepared with an anode active material meeting 0.1≤Dn10/Dv50≤0.6 has a cycle performance, rate performance and swelling resistance that are all bather than those of the lithium-ion battery prepared with an anode active material meeting Dn10/Dv50<0.1 or 0.6<Dn10/Dv50.

2. Preparation of Anode Active Material with an Oxide MeO_(y) Layer on the Surface

The anode active materials of Examples 4-12 were prepared as follows:

-   -   (1) The anode active material in Example 2, the carbon precursor         and the oxide precursor MeT_(n) were added to about 150 mL of         ethanol and about 1.47 mL of deionized water, and stirred for         about 4 hr until a uniform suspension was formed.     -   (2) The suspension was spray-dried (inlet temperature: about         220° C., outlet temperature: about 110° C.) to obtain powder.     -   (3) The powder was sintered at about 200° C. to 900° C. for         about 0.5 hr to 20 hr, to obtain an anode active material with         an oxide MeO_(y) layer on the surface.

Table 2-1 shows the process conditions for preparing the anode active materials in Examples 4-12.

TABLE 2-1 Anode active Oxide material in precursor No. Example 2 Carbon precursor MeT_(n) Sintering process Example 4 100 g Polyvinylpyrrolidone 1 g aluminum N₂ flow rate: 1.5 L/min, 2.21 g isopropoxide heating at 3° C./min to 600° C., holding for 2 hr Example 5 100 g Polyvinylpyrrolidone 1 g isopropyl N₂ flow rate: 1.5 L/min, 2.21 g titanate heating at 3° C./min to 600° C., holding for 2 hr Example 6 100 g Polyvinylpyrrolidone 0.5 g isopropyl N₂ flow rate: 1.5 L/min, 2.21 g titanate + 0.5 g heating at 3° C./min to aluminum 600° C., holding for 2 hr isopropoxide Example 7 100 g Polyvinylpyrrolidone — N₂ flow rate: 1.5 L/min, 2-21 g heating at 3° C./min to 600° C., holding for 2 hr Example 8 100 g Polyvinylpyrrolidone 5 g aluminum N₂ flow rate: 1.5 L/min, 2-21 g isopropoxide heating at 3° C./min to 600° C., holding for 2 hr Example 9 100 g Polyvinylpyrrolidone 10 g aluminum N₂ flow rate: 1.5 L/min, 2.21 g isopropoxide heating at 3° C./min to 600° C., holding for 2 hr Example 10 100 g — 1 g aluminum N₂ flow rate: 1.5 L/min, isopropoxide heating at 3° C./min to 600° C., holding for 2 hr Example 11 100 g Polyvinylpyrrolidone 1 g aluminum N₂ flow rate: 1.5 L/min, 3.31 g isopropoxide heating at 3° C./min to 600° C., holding for 2 hr Example 12 100 g Polyvinylpyrrolidone 1 g aluminum N₂ flow rate: 1.5 L/min, 6.31 g isopropoxide heating at 3° C./min to 600° C., holding for 2 hr “—” represents substance not present.

Table 2-2 and Table 2-3 show the performance test results of the anode active materials in Example 2 and Examples 4-12.

TABLE 2-2 Types Specific Capacity of Metal Carbon surface per metal content content Dv50 Dn10/ area gram * First element (wt %) (wt %) (μm) Dv50 (m²· g⁻¹) (mAh · g⁻¹) efficiency Example — — 0.030 5.0 0.5  1.42 1683 69.0% 2 Example Al 0.125% 0.300 5.1 0.51 1.45 1682 68.4% 4 Example Ti 0.125% 0.300 5.2 0.52 1.47 1678 74.0% 5 Example Al + Ti 0.125% 0.300 5.1 0.52 1.53 1682 70.3% 6 Example — 0.000% 0.300 5.2 0.51 1.38 1690 74.2% 7 Example Al 0.500% 0.300 5.3 0.52 1.98 1662 68.2% 8 Example Al 1.000% 0.300 5.4 0.53 2.40 1640 67.4% 9 Example Al 0.125% 0.000 5.1 0.52 1.43 1660 68.3% 10 Example Al 0.125% 0.500 5.2 0.52 2.01 1680 70.5% 11 Example Al 0.125% 1.000 5.1 0.52 2.42 1698 74.2% 12 “—” represents substance not present.

TABLE 2-3 Number of Number of Swelling rate cycles at cycles at of battery 25° C. 45° C. after 400 Rate No. to 90% to 80% cycles at 45° C. performance Example 2 390 375 7.9% 84.8% Example 4 500 450 7.5% 88.6% Example 5 420 392 8.0% 85.2% Example 6 433 398 8.2% 85.4% Example 7 402 388 8.1% 85.1% Example 8 520 465 7.4% 88.4% Example 9 528 468 7.2% 87.6% Example 10 490 420 7.8% 85.2% Example 11 485 402 7.9% 85.0% Example 12 463 387 7.8% 85.7%

From the test results of Example 2 and Examples 4-12, it can be seen that coating the oxide MeO_(y) layer on the anode active material that meets the condition of 0.1≤Dn10/Dv50≤0.6 can further improve the cycle performance and rate performance of the lithium-ion battery, while the first efficiency and battery swelling rate do not change significantly.

3. Preparation of an Anode Active Material with Polymer Layer on the Surface

The anode active materials of Examples 13-17 and 20-21 were prepared as follows:

-   -   (1) The carbon material (single-wall carbon nanotube (SCNT)         and/or multi-wall carbon nanotube (MCNT)) and a polymer were         dispersed in water at high speed for about 12 hr to obtain         uniformly mixed slurry;     -   (2) The anode active material in Example 4 was added to the         uniformly mixed slurry in (1) and stirred for about 4 hr to         obtain a uniformly mixed dispersion liquid; and     -   (3) The dispersion liquid was spray-dried (inlet temperature:         about 200° C., outlet temperature: about 110° C.) to obtain         powder.

The preparation method of the anode active material in Examples 18 and 19 was similar to the above method, except that the solvent in the first step of Examples 18 and 19 was N-vinylpyrrolidone.

Table 3-1 shows the compositions of the anode active materials in Examples 13-21.

TABLE 3-1 Carbon CNT Types of Polymer No. material content polymer content Example 13 SCNT 1.0 wt. %  CMC-Na 1.5 wt. % Example 14 MCNT 1.0 wt. %  CMC-Na 1.5 wt. % Example 15 SCNT:MCNT = 1.0 wt. %  CMC-Na 1.5 wt. % 1:1 (weight ratio) Example 16 SCNT 0.1 wt. %  CMC-Na 1.5 wt. % Example 17 SCNT 5 wt. % CMC-Na 1.5 wt. % Example 18 SCNT 1 wt. % PVP 1.5 wt. % Example 19 SCNT 1 wt. % PVDF 1.5 wt. % Example 20 SCNT 1 wt. % PAANa 1.5 wt. % Example 21 SCNT 1 wt. % CMC-Na  4 wt. % “—” represents substance not present.

The full names of the English abbreviations in Table 3-1 are as follows:

SCNT: Single-wall carbon nanotube

MCNT: Multi-wall carbon nanotube

CMC-Na: Sodium carboxymethyl cellulose

PVP: Polyvinylpyrrolidone

PVDF: Polyvinylidene fluoride

PAANa: Sodium polyacrylate

Table 3-2 shows the performance test results of the anode active materials in Examples 4 and 13-21.

TABLE 3-2 Number of Number of Swelling rate cycles at cycles at of battery 25° C. 45° C. after 400 Rate No. to 90% to 80% cycles at 45° C. performance Example 4 500 450 7.5% 88.6% Example 13 620 650 8.0% 89.4% Example 14 516 464 7.7% 88.7% Example 15 570 565 8.1% 88.6% Example 16 527 478 7.7% 88.2% Example 17 635 673 8.2% 89.0% Example 18 605 638 7.4% 87.8% Example 19 612 634 7.6% 87.5% Example 20 624 654 7.6% 88.5% Example 21 618 651 7.4% 83.2%

It can be seen from the test results of Example 4 and Examples 13-21 that coating a certain amount of CNT-containing polymer layer on the anode active material in Example 4 can significantly improve the cycle performance and rate performance of lithium-ion batteries.

4. The anode active materials of Examples 22-24 and Comparative Example 3 was prepared as follows:

-   -   (1) Silicon dioxide and metal silicon powder were mixed at a         molar ratio of about 1:1 through mechanical dry-mixing and         ball-milling to obtain a mixed material;     -   (2) Under an Ara atmosphere under a pressure of about 10⁻³ kPa         to 10⁻¹ kPa, the mixed material was heated for about 1-25 hr at         a temperature ranging from about 1100° C. to 1800° C. to obtain         a gas;     -   (3) The gas obtained was condensed to obtain a solid;     -   (4) The solid was crushed and screened;     -   (5) The solid was heat-treated at a temperature ranging from         about 400° C. to 1500° C. for about 0.5-24 hr under a nitrogen         atmosphere, and the heat-treated solid was cooled and graded;     -   (6) The surface of the graded solid was coated with an oxide         MeO_(y) layer containing a carbon material; for the specific         coating step, referring to the above method for preparing an         anode active material having an oxide MeO_(y) layer on the         surface; and     -   (7) The solid obtained in Step (6) was further coated with a         polymer layer containing a carbon material; for the specific         coating step, referring to the above step for preparing an anode         active material having a polymer layer on the surface.

Table 4-1 shows the specific process parameters in Steps (1)-(5), and Table 4-2 shows the specific process parameters in Step (6).

TABLE 4-1 Heating heat- Pres- temper- Heating treatment SiO₂:Si sure ature time after No. (molar ratio) (Pa) (° C.) (h) grading Example 22 1:1 10 1350 20 / Example 23 1:1 10 1350 20 600° C., 2 h Example 24 1:1 10 1350 20 800° C., 2 h Comparative 1:1 10 1350 20 1000° C., 2 h  Example 3

TABLE 4-2 Solid Oxide obtained Carbon precursor No. in Step 5 precursor MeT_(n) Sintering process Example 22 100 g Polyvinylpyrrolidone 1 g aluminum N₂ flow rate: 1.5 L/min, 2.21 g isopropoxide heating at 3° C./min to 600° C., holding for 2 hr Example 23 100 g Polyvinylpyrrolidone 1 g aluminum N₂ flow rate: 1.5 L/min, 2.21 g isopropoxide heating at 3° C./min to 600° C., holding for 2 hr Example 24 100 g Polyvinylpyrrolidone 1 g aluminum N₂ flow rate: 1.5 L/min, 2.21 g isopropoxide heating at 3° C./min to 600° C., holding for 2 hr Comparative 100 g Polyvinylpyrrolidone 1 g aluminum N₂ flow rate: 1.5 L/min, Example 3 2.21 g isopropoxide heating at 3° C./min to 600° C., holding for 2 hr

Table 4-3 shows the compositions of the anode active materials in Examples 22-24 and Comparative Example 3.

TABLE 4-3 Carbon content in Types oxide of Metal MeO_(y) CNT Polymer Dv50 = 5 μm, metal content layer CNT content Types of content Dn10/Dv50 = 0.5 I₂/I₁ element (wt %) (wt %) type (wt %) polymer (wt %) Example 22 0.41 Al 0.125 0.300 SCNT 1.0 CMC-Na 1.5 Example 23 0.64 Al 0.125 0.300 SCNT 1.0 CMC-Na 1.5 Example 24 1 Al 0.125 0.300 SCNT 1.0 CMC-Na 1.5 Comparative Example 3 2.5 Al 0.125 0.300 SCNT 1.0 CMC-Na 1.5

Table 4-4 shows the performance parameters of the lithium-ion batteries prepared with the anode active materials of Examples 22-24 and Comparative Examples 3.

TABLE 4-4 Number of Number of Swelling rate cycles at cycles at of battery 25° C. 45° C. after 400 Rate No. to 90% to 80% cycles at 45° C. performance Example 22 653 678 7.6% 90.2% Example 23 620 650 8.0% 89.4% Example 24 600 623 8.3% 88.2% Comparative 567 582 9.4% 85.2% Example 3

As can be seen from the test results of Examples 22-24 and Comparative Example 3, when the silicon oxide meets 0.1≤Dn10/Dv50≤0.6, further selecting the silicon oxide layer meeting 0<I₂/I₁≤1 to coat a metal oxide layer and a polymer layer can further improve the cycle performance and rate performance of lithium-ion batteries.

5. The anode active materials of Examples 25-27 and Comparative Example 4 were prepared as follows:

The preparation methods of the anode active materials of Examples 25-27 and Comparative Example 4 were similar to that of Examples 22-24 and Comparative Example 3, except that the preparation methods of Examples 25-27 and Comparative Example 4 do not include step (7). That is, the anode active materials of Examples 25-27 and Comparative Example 4 only had a metal oxide coating, but without a polymer coating.

Table 5-1 shows the compositions of the anode active materials in Examples 25-27 and Comparative Example 4.

TABLE 5-1 Species of Metal Carbon Dv50 = 5 μm, metal content content Dn10/Dv50 = 0.5 I₂/I₁ element (wt %) (wt %) Example 25 0.41 Al 0.125 0.300 Example 26 0.64 Al 0.125 0.300 Example 27 1 Al 0.125 0.300 Comparative 2.5 Al 0.125 0.300 Example 4

Table 5-2 shows the performance test results of the anode active materials in Examples 25-27 and Comparative Example 4.

TABLE 5-2 Number of Number of Swelling rate cycles at cycles at of battery 25° C. 45° C. after 400 Rate No. to 90% to 80% cycles at 45° C. performance Example 25 633 678 7.4 89.3% Example 26 590 650 8.2 88.4% Example 27 575 623 8.0 87.5% Comparative 532 582 9.5 86.9% Example 4

As can be seen from the test results of Examples 25-27 and Comparative Example 4, when the silicon oxide meets 0.1≤Dn10/Dv50≤0.6, further selecting the silicon oxide layer meeting 0≤I₂/I₁≤1 to coat a metal oxide layer can further improve the cycle performance and rate performance of lithium-ion batteries.

References throughout the specification to “some embodiments”, “partial embodiments”, “one embodiment”, “another example”, “example”, “specific example” or “partial examples” means that at least one embodiment or example of the application includes specific features, structures, materials or characteristics described in the embodiments or examples. Thus, the descriptions appearing throughout the specification, such as “in some embodiments”, “in an embodiment”, “in one embodiment”, “in another example”, “in an example”, “in a particular example” or “for example”, are not necessarily the same embodiment or example in the application. Furthermore, the particular features, structures, materials or characteristics herein may be combined in any suitable manner in one or more embodiments or examples.

Although illustrative embodiments have been demonstrated and described, it is to be understood by those skilled in the art that the above-mentioned embodiments cannot be construed as limitations to the present application, and that changes, replacements and modifications can be made to the embodiments without departing from the spirit, principle, and scope of the present application. 

What is claimed is:
 1. An anode material, comprising: a silicon composite substrate, wherein the Dv50 of the silicon composite substrate is from 2.5 μm to 15 μm, and a particle size distribution of the silicon composite substrate meets 0.1≤Dn10/Dv50≤0.6.
 2. The anode material according to claim 1, wherein the silicon composite substrate comprises SiO_(x), wherein 0.6≤x≤1.5.
 3. The anode material according to claim 1, wherein the silicon composite substrate comprises nano-Si crystalline grains, SiO, SiO₂, or any combination thereof.
 4. The anode material according to claim 3, wherein the silicon composite substrate comprises the nano-Si crystalline grains and the nano-Si crystalline grains have a size of less than 100 nm.
 5. The anode material according to claim 1, further comprising an oxide MeO_(y) layer, wherein the oxide MeO_(y) layer is coated on at least a portion of the silicon composite substrate, wherein Me includes at least one of Al, Si, Ti, Mn, V, Cr, Co or Zr; and y is 0.5 to 3; and wherein the oxide MeO_(y) layer comprises a carbon material.
 6. The anode material according to claim 5, wherein a thickness of the oxide MeO_(y) layer is 1 nm to 1000 nm.
 7. The anode material according to claim 5, wherein based on a total weight of the anode material, a content of the Me element is 0.01 wt % to 1 wt %.
 8. The anode material according to claim 5, wherein based on a total weight of the anode material, a content of the carbon material in the oxide MeO_(y) layer is 0.05 wt % to 1 wt %.
 9. The anode material according to claim 5, further comprising a polymer layer, wherein the polymer layer is coated on at least a portion of the oxide MeO_(y) layer, wherein the polymer layer comprises a carbon material.
 10. The anode material according to claim 9, wherein the polymer layer comprises polyvinylidene fluoride and derivatives of the polyvinylidene fluoride, carboxymethyl cellulose and derivatives of the carboxymethyl cellulose, sodium carboxymethyl cellulose and derivatives of sodium carboxymethyl cellulose, polyvinylpyrrolidone and derivatives of polyvinylpyrrolidone, polyacrylic acid and derivatives of polyacrylic acid, polystyrene-butadiene rubber, polyacrylamide, polyimide, polyamideimide or any combination thereof.
 11. The anode material according to claim 5, wherein the carbon material comprises carbon nanotubes, carbon nanoparticles, carbon fibers, graphene, or any combination thereof.
 12. The anode material according to claim 9, wherein based on a total weight of the anode material, a content of the polymer layer is 0.1 wt % to 10 wt %.
 13. The anode material according to claim 9, wherein a thickness of the polymer layer is 2 nm to 100 nm.
 14. The anode material according to claim 5, wherein in the X-ray diffraction pattern, the highest intensity at 2θ within the range of 27.0° to 30.0° is I₂, and the highest intensity at 2θ within the range of 20.0° to 22.0° is I₁, wherein 0≤I₂/I₁≤1.
 15. The anode material according to claim 9, wherein in the X-ray diffraction pattern, the highest intensity at 2θ within the range of 27.0° to 30.0° is I₂, and the highest intensity at 2θ within the range of 20.0° to 22.0° is I₁, wherein 0≤I₂/I₁≤1.
 16. The anode material according to claim 1, wherein the anode material has a specific surface area of 1 to 50 m²/g.
 17. An anode comprising an anode material, the anode material comprises a silicon composite substrate, wherein the Dv50 of the silicon composite substrate is from 2.5 μm to 15 μm, and a particle size distribution of the silicon composite substrate meets 0.1≤Dn10/Dv50≤0.6.
 18. An electrochemical device, wherein the electrochemical device comprises an anode according to claim
 17. 19. An electronic device, wherein the electronic device comprises an electrochemical device according to claim
 18. 